RU2009121628A - Реакторная система для получения газообразных продуктов - Google Patents
Реакторная система для получения газообразных продуктов Download PDFInfo
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Abstract
1. Прямоточный реактор с нисходящими потоками для превращения жидкого исходного сырья в неконденсирующийся газообразный продукт с использованием гетерогенного катализатора, включающий ! реакционную камеру, содержащую по меньшей мере одну реакционную трубку, содержащую гетерогенный катализатор; ! входное отверстие, давление в котором равно Pi, выполненное с возможностью подавать жидкий питающий поток в верхнюю часть реакционной камеры; ! выходное отверстие, давление в котором равно Ро, выполненное с возможностью выпускать неконденсирующийся газообразный продукт и жидкий выходящий поток из нижней части реакционной камеры; и ! в котором Pi больше, чем Ро. ! 2. Реактор по п.1, в котором реакционная камера включает ряд реакционных трубок, каждая из которых содержит катализатор, внешнюю оболочку, выполненную с возможностью заключать в себе по меньшей мере часть реакционных трубок, и систему нагрева, выполненную с возможностью вводить теплоноситель внутрь оболочки для осуществления нагревания реакционных трубок. ! 3. Реактор по п.1, в котором катализатор включает по меньшей мере один металл группы VIIIВ, и в котором исходное сырье включает воду и по меньшей мере один растворимый в воде кислородсодержащий С2+ углеводород. ! 4. Реактор по п.3, в котором металл группы VIIIB выбирают из группы, состоящей из платины, никеля, палладия, рутения, родия, иридия, железа, их сплавов и их смесей, и в котором кислородсодержащий углеводород представляет собой кислородсодержащий С2-6 углеводород. ! 5. Реактор по п.4, в котором катализатор дополнительно включает второй каталитический материал, выбранный из группы, состоящей из металлов групп�
Claims (21)
1. Прямоточный реактор с нисходящими потоками для превращения жидкого исходного сырья в неконденсирующийся газообразный продукт с использованием гетерогенного катализатора, включающий
реакционную камеру, содержащую по меньшей мере одну реакционную трубку, содержащую гетерогенный катализатор;
входное отверстие, давление в котором равно Pi, выполненное с возможностью подавать жидкий питающий поток в верхнюю часть реакционной камеры;
выходное отверстие, давление в котором равно Ро, выполненное с возможностью выпускать неконденсирующийся газообразный продукт и жидкий выходящий поток из нижней части реакционной камеры; и
в котором Pi больше, чем Ро.
2. Реактор по п.1, в котором реакционная камера включает ряд реакционных трубок, каждая из которых содержит катализатор, внешнюю оболочку, выполненную с возможностью заключать в себе по меньшей мере часть реакционных трубок, и систему нагрева, выполненную с возможностью вводить теплоноситель внутрь оболочки для осуществления нагревания реакционных трубок.
3. Реактор по п.1, в котором катализатор включает по меньшей мере один металл группы VIIIВ, и в котором исходное сырье включает воду и по меньшей мере один растворимый в воде кислородсодержащий С2+ углеводород.
4. Реактор по п.3, в котором металл группы VIIIB выбирают из группы, состоящей из платины, никеля, палладия, рутения, родия, иридия, железа, их сплавов и их смесей, и в котором кислородсодержащий углеводород представляет собой кислородсодержащий С2-6 углеводород.
5. Реактор по п.4, в котором катализатор дополнительно включает второй каталитический материал, выбранный из группы, состоящей из металлов группы VIIIB, металлов группы VIIB, металлов группы VIB, металлов группы VB, металлов группы IVB, металлов группы IIB, металлов группы IB, металлов группы IVA, металлов группы VA, их сплавов и их смесей.
6. Реактор по п.5, в котором второй каталитический материал представляет собой рений, а переходный металл группы VIIIB выбран из группы, состоящей из железа, никеля, палладия, платины, рутения, родия, их сплавов и их смесей.
7. Реактор по п.3, в котором катализатор нанесен на носитель, изготовленный из одного или более материалов, выбранных из группы, состоящей из углерода, оксида кремния, оксида кремния-оксида алюминия, оксида алюминия, оксида циркония, оксида титана, оксида церия, оксида ванадия и их смесей.
8. Реактор по п.1, в котором неконденсирующийся газообразный продукт включает один или более газов, выбранных из группы, состоящей из водорода, диоксида углерода, моноксида углерода, метана, этана, этилена, пропана, пропилена, бутана, бутена, пентана и пентена.
9. Система получения электроэнергии, включающая любой из реакторов по пп.1-8 и устройство для получения электроэнергии, способное использовать неконденсирующийся газообразный продукт в качестве топлива.
10. Система получения электроэнергии по п.9, в которой устройство для получения электроэнергии представляет собой элемент, выбранный из группы, состоящей из двигателя внутреннего сгорания, топливного элемента с протонообменной мембраной, топливного элемента на основе твердых оксидов и генераторной установки с газовой турбиной.
11. Способ получения неконденсирующегося газа, включающий проведение реакции жидкого исходного сырья, содержащего воду и по меньшей мере один водорастворимый кислородсодержащий С2+ углеводород, с использованием гетерогенного катализатора, содержащего один или более металлов группы VIIIB, при температуре примерно от 80 до 300°С и давлении реакции, пригодном для получения неконденсирующегося газа и жидкого выходящего потока, в котором градиент давления обеспечивает течение жидкого исходного сырья, выходящего жидкого потока и неконденсирующегося газа прямотоком в направлении сверху вниз.
12. Способ по п.11, в котором металл группы VIIIB выбран из группы, состоящей из платины, никеля, палладия, рутения, родия, иридия, железа, их сплавов и их смесей.
13. Способ по п.11, в котором катализатор дополнительно включает второй каталитический материал, выбранный из группы, состоящей из металлов группы VIIB, металлов группы VIB, металлов группы VB, металлов группы IVB, металлов группы IIВ, металлов группы IB, металлов группы IVA, металлов группы VA, их сплавов и их смесей.
14. Способ по п.13, в котором второй каталитический материал представляет собой рений, а металл группы VIIIB выбран из группы, состоящей из железа, никеля, палладия, платины, рутения, родия, их сплавов и их смесей.
15. Способ по п.11, в котором катализатор нанесен на носитель, изготовленный из одного или более материалов, выбранных из группы, состоящей из углерода, оксида кремния, оксида кремния-оксида алюминия, оксида алюминия, оксида циркония, оксида титана, оксида церия, оксида ванадия и их смесей.
16. Способ по п.11, в котором кислородсодержащий углеводород представляет собой кислородсодержащий C1-6 углеводород.
17. Способ по п.16, в котором кислородсодержащий углеводород представляет собой вещество, выбранное из группы, состоящей из сахара и сахарного спирта.
18. Способ по п.11, в котором температура реакции составляет от примерно 150°С до примерно 270°С, а давление реакции составляет от примерно 0,494 МПа до примерно 8,92 МПа (от 72 до 1300 избыт. фунтов на кв. дюйм).
19. Способ по п.11, включающий использование любого из реакторов по пп.1-8.
20. Способ по п.11, в котором неконденсирующийся газ включает один или более газов, выбранных из группы, состоящей из водорода, диоксида углерода, моноксида углерода, метана, этана, этилена, пропана, пропилена, бутана, бутена, пентана и пентена.
21. Способ по п.11, в котором градиент давления находится в диапазоне от 3,43 до 20,58 кПа (от 0,5 до 3 избыт. фунтов на кв. дюйм).
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-
2007
- 2007-12-20 BR BRPI0719504A patent/BRPI0719504A2/pt not_active IP Right Cessation
- 2007-12-20 WO PCT/US2007/088417 patent/WO2008140617A2/en active Application Filing
- 2007-12-20 CA CA002671730A patent/CA2671730A1/en not_active Abandoned
- 2007-12-20 RU RU2009121628/05A patent/RU2009121628A/ru not_active Application Discontinuation
- 2007-12-20 AU AU2007353527A patent/AU2007353527B2/en active Active
- 2007-12-20 KR KR1020097015061A patent/KR20090101260A/ko not_active Application Discontinuation
- 2007-12-20 NZ NZ577547A patent/NZ577547A/en unknown
- 2007-12-20 CN CNA2007800477165A patent/CN101568377A/zh active Pending
- 2007-12-20 US US11/961,280 patent/US20100288975A1/en not_active Abandoned
- 2007-12-20 JP JP2009543232A patent/JP2010514548A/ja active Pending
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- 2007-12-20 EP EP07874380A patent/EP2111291A2/en not_active Withdrawn
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- 2009-07-21 CO CO09075423A patent/CO6210746A2/es not_active Application Discontinuation
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Also Published As
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MX2009006509A (es) | 2009-10-28 |
JP2010514548A (ja) | 2010-05-06 |
US8834587B2 (en) | 2014-09-16 |
WO2008140617A3 (en) | 2009-01-15 |
CN101568377A (zh) | 2009-10-28 |
NZ577547A (en) | 2012-05-25 |
US20100288975A1 (en) | 2010-11-18 |
CO6210746A2 (es) | 2010-10-20 |
BRPI0719504A2 (pt) | 2017-10-24 |
WO2008140617A2 (en) | 2008-11-20 |
KR20090101260A (ko) | 2009-09-24 |
AU2007353527A1 (en) | 2008-11-20 |
ZA200904056B (en) | 2010-04-28 |
EP2111291A2 (en) | 2009-10-28 |
US20120282163A1 (en) | 2012-11-08 |
CA2671730A1 (en) | 2008-11-20 |
AU2007353527B2 (en) | 2012-12-20 |
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